WO2010061512A1

WO2010061512A1 - Centrifugal compressor

Info

Publication number: WO2010061512A1
Application number: PCT/JP2009/005046
Authority: WO
Inventors: 堀江茂斉; 得山伸一郎
Original assignee: 三菱重工業株式会社
Priority date: 2008-11-28
Filing date: 2009-09-30
Publication date: 2010-06-03
Also published as: JP2010127245A

Abstract

A centrifugal compressor provided with a casing, a rotating shaft supported in the casing, an impeller provided to the rotating shaft and compressing a fluid, and a cleaning liquid ejecting device for ejecting a cleaning liquid into a flow path formed by the impeller and the casing. The liquid ejecting device is provided with a first ejecting section for ejecting the cleaning liquid from circumferentially spaced points toward the gap between a small-diameter section of the casing and the impeller, and also with a second ejecting section for ejecting the cleaning liquid from circumferentially spaced points from the upstream side of the fluid, which has been compressed by the impeller, toward the downstream side.

Description

Centrifugal compressor

The present invention relates to a centrifugal compressor.
This application claims priority based on Japanese Patent Application No. 2008-305138 for which it applied to Japan on November 28, 2008, and uses the content here.

As is well known, one type of centrifugal compressor used in various plants and the like injects a cleaning liquid into a flow path. In this type of centrifugal compressor, dirt and thermal reaction products adhering / depositing on the flow path are removed, so that the performance deteriorated by the adhering matter / deposit can be recovered. Moreover, since gas temperature falls by vaporization of a washing | cleaning liquid, drive power can be reduced and generation | occurrence | production of the said thermal reaction product can be suppressed.

For example, in Patent Document 1 below, a rotating shaft supported in a casing, a plurality of impellers that rotate together with the rotating shaft, a diffuser having a diffuser vane that is a downstream portion of the impeller, and a diffuser A liquid injection nozzle for ejecting evaporable liquid into the gas flow path is provided on the casing wall on the core plate side of at least one stage of the impeller. A centrifugal compressor is disclosed.

Japanese Patent No. 2918773

However, in the prior art, since the liquid injection nozzle is provided on the casing wall surface on the core plate side of the impeller, the cleaning liquid that has flowed out from the outermost peripheral portion of the impeller to the flow path radially outward is impeller in the axial direction. There is a problem that the distribution of the cleaning liquid is not uniform because the vehicle is biased toward the large diameter side rather than the small diameter side.
In addition, since the distribution of the cleaning liquid is not uniform, it is not economical because it is necessary to inject cleaning liquid more than necessary without completely removing dirt and the like adhering to and accumulated in the flow path. There is a problem that the mixing ratio of the cleaning liquid increases.

In view of the above problems, the present invention has the following objects.
(1) Distribute the cleaning liquid uniformly in the flow path.
(2) It uniformly removes and suppresses dirt and thermal reaction products adhering / depositing on the flow path, and obtains a cooling effect uniformly.
(3) The mixing ratio of the cleaning liquid to the fluid is reduced using the minimum necessary cleaning liquid.

In order to achieve the above object, the present invention employs the following means.
That is, the present invention provides a casing, a rotating shaft supported in the casing, an impeller provided on the rotating shaft for compressing a fluid, and a cleaning liquid is injected into a flow path formed by the impeller and the casing. A centrifugal compressor including a cleaning liquid ejecting apparatus, wherein the liquid ejecting apparatus ejects the cleaning liquid from a plurality of locations in a circumferential direction toward a gap between the small diameter portion of the casing and the impeller; A second injection unit that injects the cleaning liquid from a plurality of locations in the circumferential direction from the upstream side to the downstream side of the fluid compressed by the impeller.

According to this configuration, the first injection unit that injects the cleaning liquid from a plurality of locations in the circumferential direction toward the gap between the small diameter portion of the casing and the impeller, and the periphery of the fluid compressed by the impeller from the upstream side toward the downstream side. Since the second ejection unit that ejects the cleaning liquid from a plurality of locations in the direction is provided, the cleaning liquid can be uniformly distributed in the flow path.
That is, since the first injection unit directly injects the cleaning liquid immediately before the impeller entrance, in the axial direction, the ratio of the cleaning liquid reaching from the impeller entrance to the outermost peripheral portion (outlet) of the impeller increases, and the cleaning liquid is transferred to the entire impeller. And can be distributed downstream.
On the other hand, since the second injection unit injects the cleaning liquid from the upstream side to the downstream side of the fluid compressed by the impeller, the cleaning liquid flows in the axial direction without colliding or adhering to the casing. Thereby, generation | occurrence | production of the erosion by the washing | cleaning liquid colliding with a casing is suppressed, and a washing | cleaning liquid can be efficiently spread | distributed in the downstream of an impeller.
Furthermore, since the first injection unit and the second injection unit inject the cleaning liquid from a plurality of locations, the cleaning liquid can be spread over the entire impeller in the circumferential direction.
Therefore, the cleaning liquid can be uniformly distributed with respect to the flow path.
Therefore, dirt and thermal reaction products adhering to and depositing on the flow path can be removed and suppressed uniformly, and a cooling effect can be obtained uniformly. In addition, since the cleaning liquid can be uniformly distributed in the flow path, the mixing ratio of the cleaning liquid to the gas can be reduced without using the cleaning liquid unnecessarily.

The first injection unit may include a radial injection body that injects the cleaning liquid in a radial direction toward the gap.
According to this configuration, since the first injection unit includes the radial injection body that injects the cleaning liquid in the radial direction, the cleaning liquid piping can be configured to be short, and the small-diameter portion of the casing and the impeller can be configured with a simple configuration. The cleaning liquid can be sprayed toward the gap. Furthermore, since the refinement of particles by shearing proceeds at the bent portion of the impeller inlet, the generation of erosion can be suppressed and the flow of the fluid can be easily accompanied.

In addition, the tip position of the first injection part is arranged in the radial direction and is biased toward the outer peripheral side of the impeller, and the first injection part injects the cleaning liquid in the axial direction toward the gap. You may have a body.
According to this configuration, the distal end position of the first injection unit is arranged in the radial direction so as to be biased toward the outer peripheral side of the impeller, and the first injection unit includes the axial injection body that injects the cleaning liquid in the axial direction. Therefore, the cleaning liquid can easily reach the outer peripheral side of the impeller regardless of the inertia in the axial direction when the fluid passes through the impeller.

The second injection unit may include an oblique injection body that injects the cleaning liquid in a direction obliquely intersecting with the fluid that flows radially outward from the outermost peripheral portion of the impeller.
According to this configuration, the second injection unit includes the oblique direction injection body that injects the cleaning liquid in a direction obliquely intersecting with the fluid that flows radially outward from the outermost peripheral portion of the impeller. The cleaning liquid can be directly sprayed in the vicinity of the impeller outlet where the temperature rises rapidly and there are many thermal reaction products. Thereby, a cleaning effect and a cooling effect can be heightened efficiently.

A plurality of the impellers are provided in the axial direction, and the casing has a return bend portion that directs the fluid that flows radially outward from the upstream impeller toward the downstream impeller adjacent to the upstream impeller. Is formed, and the fluid is compressed in multiple stages, and the second injection unit is provided on the downstream side of the return bend unit, and returns bend injection that injects the cleaning liquid radially inward. You may have a body.
According to this configuration, the second injection part is provided on the downstream side of the return bend part and includes the return bend injection body that injects the cleaning liquid radially inward, so that the cleaning liquid does not collide or adhere to the casing. It flows to the flow path that goes radially inward. Thereby, generation | occurrence | production of the erosion by the washing | cleaning liquid colliding with a casing is suppressed, and a washing | cleaning liquid can be efficiently spread | circulated in the flow path which goes to radial inside.

Further, at least one of the first injection unit and the second injection unit may spray the cleaning liquid.
According to this configuration, since at least one of the first injection unit and the second injection unit sprays the cleaning liquid, it is possible to further enhance the effect of suppressing the occurrence of erosion.

The casing, a rotating shaft supported in the casing, a plurality of impellers provided on the rotating shaft for compressing fluid, and the plurality of impellers in a flow path formed by the plurality of impellers and the casing. The centrifugal compressor includes a plurality of injectors that are provided on the upstream side of each of the nozzles and injects the cleaning liquid, and a control unit that adjusts the injection amount of each of the injectors, and the control unit is located on the upstream side Each of the injection amounts may be gradually decreased toward the injector located downstream from the injector.
According to this configuration, the control unit gradually decreases each injection amount from the injection body located on the upstream side toward the injection body located on the downstream side, so that the temperature rise of the fluid is large and the thermal reaction is generated. A large amount of cleaning liquid is injected to the upstream side where there are many objects, and a small amount of cleaning liquid is injected to the downstream side where the temperature rise is small. Accordingly, since the cleaning liquid is ejected according to the required amount of the cleaning liquid in each part of the flow path, the mixing ratio of the cleaning liquid to the fluid can be reduced without using the cleaning liquid unnecessarily.

The control unit may limit the total amount of the cleaning liquid ejected from each of the ejectors to a predetermined ratio with respect to the amount of the fluid.
According to this configuration, since the control unit limits the total amount of the cleaning liquid to a predetermined ratio with respect to the amount of fluid, the mixing ratio of the cleaning liquid to the fluid is limited to a predetermined range to obtain a fluid having a desired quality. Can do.

According to the present invention, the cleaning liquid can be uniformly distributed in the flow path. Further, it is possible to uniformly remove and suppress dirt and thermal reaction products adhering / depositing on the flow path, and to obtain a uniform cooling effect. Furthermore, the mixing ratio of the cleaning liquid to the fluid can be reduced by using the minimum necessary cleaning liquid.

It is a schematic structure sectional view of centrifugal compressor A concerning a first embodiment of the present invention. It is principal part sectional drawing of the centrifugal compressor A which concerns on 1st embodiment of this invention. It is an II line (II-II line, III-III line) sectional view of centrifugal compressor A concerning a first embodiment of the present invention. It is principal part sectional drawing which shows the 1st modification of the centrifugal compressor A which concerns on 1st embodiment of this invention. It is principal part sectional drawing which shows the 2nd modification of the centrifugal compressor A which concerns on 1st embodiment of this invention. It is a schematic structure sectional view of centrifugal compressor B concerning a first embodiment of the present invention.

Embodiments of the present invention will be described below with reference to the drawings.
(First embodiment)
FIG. 1 is a schematic cross-sectional view of a centrifugal compressor A according to the first embodiment of the present invention.
As shown in FIG. 1, the centrifugal compressor A is used for compression of an ethylene raw material gas E, and includes a casing 1 in which intake ports 2A and 2B and an outlet 3 of the ethylene raw material gas E are formed, The shaft is supported by the bearings 4A and 4B, the rotating shaft 5 is inserted through the casing 1, the plurality of impellers 6 attached to the rotating shaft 5, and the ethylene raw material composed of the plurality of impellers 6 and the casing 1. A cleaning liquid spraying device 20 that sprays the cleaning liquid W is provided in the flow path of the gas E.

The centrifugal compressor A is a type in which the arrangement type of the impellers 6 is referred to as a rear arrangement. Specifically, the three impellers 6 are arranged on one end side of the rotating shaft 5 and the small diameter side is directed to one end side. Three impellers 6 are arranged on the other end side in the axial direction with the small diameter side facing the other end.
That is, the centrifugal compressor A compresses the ethylene raw material gas E sucked from the suction ports 2A and 2B formed at both ends of the casing 1 at one end side and the other end side inside the

casing

1, 1 is discharged from a discharge port 3 formed at the center of 1.

As shown in FIG. 1, the casing 1 has an internal space in which the diameter reduction and the diameter increase are repeated from the

introduction portions

1 a and 1 b communicating with the suction ports 2 A and 2 B to the discharge portion 1 c communicating with the discharge port 3, respectively. The rotating shaft 5 and the impeller 6 are accommodated in this internal space. The casing 1 forms two compression flow paths R for the ethylene raw material gas E together with the impeller 6 on both sides in the axial direction. The compression flow path R will be described later.

FIG. 2 is a cross-sectional view of a main part of the centrifugal compressor A. In the following description, one of the two compression channels R will be described, but the other has the same configuration.
The impeller 6 has a plurality of blades 6b formed on a hub 6a formed so as to gradually increase in diameter as it advances to one side in the axial direction, and the shurad 6c is joined so as to cover the outer peripheral portion of the blade 6b in the circumferential direction. It has been configured.

The compression flow path R compresses the ethylene raw material gas E in three stages, and includes a suction passage 11, a compression passage 12, a diffuser passage 13, a return bend passage 14, and a return passage 15.

The suction passage 11 is defined by a gap between each impeller 6 (hub 6a) and the small diameter portion 1d of the casing 1 and communicates with the compression passage 12. The suction passage 11 on the upstream side of the impeller 6 in the first stage (shaft end side) communicates with the introduction portion 1a.

The compression passage 12 is defined by the blade mounting surface of the hub 6a and the inner wall surface of the shurad 6c.
The diffuser passage 13 is defined by a diffuser front wall 13 a of the casing 1 and a diffuser rear wall 13 b of a partition wall member 1 e attached to the casing 1. As for this diffuser channel | path 13, the 1st step and the 2nd step are connected to the return bend channel | path 14, and the 3rd step is connected to the discharge part 1c (refer FIG. 1).

The return bend passage 14 is defined by the inversion passage wall 14a of the casing 1 and the outer peripheral end wall 14b of the partition wall member 1e. The return bend passage 14 communicates with the return passage 15.

The return passage 15 is defined by a downstream side wall 15a of the partition wall member 1e and an upstream side wall 15b formed integrally with the casing 1 and extending toward the inner peripheral side. The first-stage return passage 15 is divided by return vanes 15c. The return passage 15 communicates with the second and third suction passages 11.

With such a configuration, the ethylene source gas E passes through the compression flow path R through the first-stage suction passage 11, the compression passage 12, the diffuser passage 13, the return bend passage 14, the return passage 15, and the second stage from the introduction portion 1 b. The suction passage 11, the compression passage 12, the diffuser passage 13, the return bend passage 14, the return passage 15, the third-stage suction passage 11, the compression passage 12, the diffuser passage 13, and the discharge portion 1c are sequentially flowed and compressed. The

As shown in FIG. 1, the cleaning liquid spraying device 20 sprays the cleaning liquid W onto the compression flow path R, and includes a first spraying part 21 and a second spraying part 22.

As shown in FIG. 3, the first spray unit 21 includes four radial spray bodies 21 a arranged in the introduction unit 1 b.
The four radial spray bodies 21a are annularly arranged at equal intervals around the axis P, and each of the cleaning liquids W is directed radially inward from the radially outward toward the first-stage suction passage 11. Spray. More specifically, each radial spray body 21a sprays at an injection angle of about 115 degrees in a cross section orthogonal to the axis P so that a part of the radial spray body 21a overlaps with the adjacent radial spray body 21a.
The radial spray body 21a includes a pipe that penetrates the casing 1 and a nozzle that can spray the cleaning liquid W.

The second spray section 22 includes a return bend spray body 22a embedded in a reversing passage wall 14a constituting the first and second stage return bend passages 14.
As shown in FIG. 3, four return bend spray bodies 22a are annularly arranged at equal intervals on the downstream side (exit side) of the first-stage and second-stage reversing passage walls 14a.

The return bend spray body 22a is composed of a pipe penetrating the casing 1 and a nozzle capable of spraying the cleaning liquid W, like the radial spray body 21a. The return bend spray body 22a is directed from the upstream side to the downstream side of the ethylene raw material gas E, in other words, toward the ethylene raw material gas E whose flow direction is changed radially inward through the return bend passage 14. The direction of the nozzle is set so as to spray the cleaning liquid W.

The cleaning liquid spraying device 20 having such a configuration is filled with a solvent that dissolves the polymer produced as the temperature of the ethylene raw material gas E increases as the cleaning liquid W.

Next, a method for cleaning the centrifugal compressor A having the above-described configuration will be described.
First, the centrifugal compressor A is driven, and the ethylene raw material gas E is sequentially compressed through the compression flow path R. That is, when the ethylene raw material gas E passes through the compression passage 12 (impeller 6), the velocity energy and the pressure energy increase. When the ethylene raw material gas E passes through the diffuser passage 13 thereafter, the velocity energy is converted into pressure energy and pressure. Will increase. At this time, the range of pressure increase of the ethylene source gas E is the largest in the first stage and the smallest in the third stage.

The temperature of the ethylene raw material gas E rises with the pressure increase in each stage. That is, the temperature increase range of the ethylene source gas E is the largest in the first stage and the smallest in the third stage.
As the ethylene source gas E rises in temperature, a polymer is generated from the ethylene source gas E and adheres to the casing 1 and the impeller 6. At this time, the degree of polymer adhesion is the highest in the first stage, and the diffuser passage 13 (especially the inlet side) is the highest in each stage.
As the polymer accumulates, the flow rate and pressure of the ethylene raw material gas E discharged from the discharge port 3 decrease.

In order to remove the polymer, the cleaning liquid spray device 20 sprays the cleaning liquid W from the first spray body 21 and the second spray section 22 onto the compression flow path R. Most of the sprayed cleaning liquid W is atomized and accompanies the flow of the ethylene raw material gas E.

More specifically, when the cleaning liquid W sprayed radially inward from the radial spray body 21a of the first spray body 21 flows into the first-stage suction passage 11 from the introduction portion 1b, the ethylene raw material As the gas E flows, the flow direction is changed from the radial direction to the axial direction. At this time, the liquid cleaning liquid W is refined by shearing, and reaches the compression passage 12, the diffuser passage 13, and the return bend passage 14. In addition, since the radial spray bodies 21 are annularly arranged at equal intervals and spray the cleaning liquid W, the cleaning liquid W spreads in the circumferential direction. In this way, the cleaning liquid W that reaches the compression passage 12 and the diffuser passage 13 dissolves and removes the deposited polymer and flows downstream.

The cleaning liquid W sprayed from the return bend spray body 22a of the second spray section 22 is accompanied by the ethylene source gas E that has changed its flow direction radially inward through the return bend passage 14, and the partition member 1e It flows downstream without colliding or adhering to the outer peripheral end wall 14b.
Then, the air flows into the second-stage and third-stage compression passages 12 (impellers 6) through the return passages 15, and flows into the second-stage and third-stage diffuser passages 13, respectively. Moreover, since the return bend spray bodies 22a are annularly arranged at equal intervals and spray the cleaning liquid W, the cleaning liquid W is distributed in the circumferential direction. In this way, the cleaning liquid W that has spread over the return path 15, the second stage, the third stage compression path 12, and the second stage, third stage diffuser path 13 is used to remove the deposited polymer. It dissolves and removes and flows downstream.

The centrifugal compressor A from which the accumulated polymer has been removed recovers the flow rate and pressure of the ethylene raw material gas E discharged from the discharge port 3. Thereafter, the centrifugal compressor A stops spraying the cleaning liquid W of the cleaning liquid spraying device 20 and continues stable operation.

As described above, according to the centrifugal compressor A, the first spraying portion 21 that sprays the cleaning liquid W from a plurality of locations in the circumferential direction toward the gap between the small diameter portion 1 d of the casing 1 and the impeller 6, and the impeller 6 Since the compressed ethylene raw material gas E is provided with the second spraying portion 22 that sprays the cleaning liquid W from a plurality of locations in the circumferential direction from the upstream side to the downstream side, the cleaning liquid W is uniformly distributed with respect to the compression flow path R. Can be made.
That is, since the first spray portion 21 sprays the cleaning liquid W directly immediately before the impeller 6, the ratio of the cleaning liquid W reaching the compression passage 12, the diffuser passage 13, and the return bend passage 14 in the axial direction increases. The cleaning liquid W can be distributed to the compression passage 12, the diffuser passage 13, and the return bend passage 14.

On the other hand, since the second spray part 22 sprays the cleaning liquid W from the upstream side to the downstream side of the ethylene raw material gas E compressed by the impeller 6, the cleaning liquid W in the axial direction is the outer peripheral end wall 14b of the partition wall member 1e. It flows downstream without colliding or adhering to. As a result, the occurrence of erosion due to the collision of the cleaning liquid W with the casing 1 is suppressed, and the second and third stage compression passages 12 (impeller 6) and the first stage are connected via the return passage 15 of the impeller 6. The cleaning liquid W can be efficiently distributed to the second-stage and third-stage diffuser passages 13.
Furthermore, since the 1st spray part 21 and the 2nd spray part 22 spray the washing | cleaning liquid W at equal intervals in the circumferential direction, a washing | cleaning liquid can be spread over the whole impeller.
Therefore, the cleaning liquid W can be uniformly distributed to the compression flow path R.
Therefore, dirt and thermal reaction products adhering to and accumulating in the compression flow path R can be uniformly removed and suppressed. Furthermore, the cooling effect can be obtained uniformly. Further, since the cleaning liquid W can be uniformly distributed in the compression flow path R, the mixing ratio of the cleaning liquid W to the gas can be reduced without using the cleaning liquid W unnecessarily.

Further, since the first spray portion 21 includes the axial spray body 21a that sprays the cleaning liquid W in the radial direction, the piping of the cleaning liquid W can be configured to be short, and the small-diameter portion 1d of the casing 1 and the impeller can be configured with a simple configuration. It becomes possible to spray the cleaning liquid W toward the gap with 6. Furthermore, since the refinement of particles by shearing proceeds at the bend of the impeller inlet, the generation of erosion can be suppressed and the flow of the ethylene source gas E can be easily accompanied.

Moreover, since the first spraying part 21 and the second spraying part 22 spray the cleaning liquid W, the effect of suppressing the occurrence of erosion can be further enhanced.

Subsequently, modified examples (first modified example, second modified example) of the above-described first embodiment will be described with reference to the drawings. In the following description, the same components as those shown in FIGS. 1 to 3 are given the same reference numerals, and the description thereof is omitted.

FIG. 4 is a cross-sectional view of a main part showing a first modification of the centrifugal compressor A.
In the first modification, as shown in FIG. 4, the configuration of the first spray unit 21 is changed to the axial spray body 21b instead of the radial spray body 21a described above.
The four axial spray bodies 21b are annularly arranged at four equal intervals around the axis P in the introduction portion 1b, and spray the cleaning liquid W in the axial direction toward the first suction passage 11 respectively.
More specifically, each axial spray body 21 b has a pipe extending to a position overlapping the impeller 6 in the radial direction, and sprays the cleaning liquid W in the axial direction toward the suction passage 11. Here, the tip positions of the axial spray bodies 21b are arranged in the radial direction so as to be biased toward the outer peripheral side of the impeller.

According to this configuration, since the first spray unit 21 includes the axial spray body that sprays the cleaning liquid in the axial direction, the fluid is also applied to the outer peripheral side of the impeller regardless of the inertia toward the axial direction when the fluid passes through the impeller. The cleaning liquid can be easily reached.
That is, when the ethylene raw material gas E passes from the suction passage 11 through the compression passage 12, a gas flow is formed that is directed radially outward. On the other hand, if the cleaning liquid W accompanies the ethylene source gas E, inertia acts in the axial direction.
However, according to this configuration, since the axial spray body 21b that sprays the cleaning liquid W in the axial direction is arranged in the radial direction and biased toward the outer periphery of the impeller, the cleaning liquid W is a gas that goes outward in the radial direction. The cleaning liquid W can easily reach the outer peripheral side of the compression passage 12 without mixing with the flow and drifting in the axial direction. That is, since the first spraying part 21 sprays the cleaning liquid W directly toward the gap between the small diameter part 1d of the casing 1 and the impeller 6 immediately before the impeller 6, in the axial direction, the compression passage 12, the diffuser passage 13, and The ratio of the cleaning liquid W that reaches the return bend passage 14 increases, and the cleaning liquid W can be distributed to the compression passage 12, the diffuser passage 13, and the return bend passage 14.

Then, the 2nd modification of 1st embodiment mentioned above is demonstrated.
FIG. 5 is a cross-sectional view of a main part showing a second modification of the centrifugal compressor A.
In the second modification, the configuration of the second spray unit 22 is changed to the oblique spray body 22b instead of the return bend spray body 22a described above.

The oblique spray bodies 22b are annularly arranged at four equal intervals around the axis P on each diffuser front wall 13a, and each of the oblique spray bodies 22b is inclined obliquely from the upstream side to the downstream side of the ethylene raw material gas E flowing through the diffuser passage 13. The cleaning liquid W is sprayed in the intersecting direction.

According to this configuration, it is possible to spray the cleaning liquid W directly in the vicinity of the outlet of the compression passage 12 (in the vicinity of the inlet of the diffuser passage 13) where the temperature of the ethylene raw material gas E is so high that a large amount of polymer is generated. Thereby, a cleaning effect and a cooling effect can be heightened efficiently.

In addition, it may replace with said structure and you may equip the 1st spraying part 21 with the radial direction spray body 21a and the axial direction spray body 21b simultaneously. Similarly, you may equip the 2nd spraying part 22 with the return bend spray body 22a and the diagonal spray body 22b simultaneously.

(Second embodiment)
Next, a second embodiment of the present invention will be described.
FIG. 6 is a schematic cross-sectional view of a centrifugal compressor B according to the second embodiment of the present invention.
As illustrated in FIG. 6, the centrifugal compressor B includes a centrifugal compressor body 40 having the same configuration as the centrifugal compressor A described above, and a flow rate controller (control unit) 50 that adjusts the spray amount of the cleaning liquid W. Yes.

Each radial spray body 21a and each return bend spray body 22a are connected to the same cleaning liquid tank T via a pipe, and each has an electric valve 51 and a pressure sensor 52 for detecting the original pressure of the nozzle. Is provided.
The cleaning liquid W is pumped from the cleaning liquid tank T to the pipes of the radial spray bodies 21a and the return bend spray bodies 22a. In addition, the pressure exceeding the pressure of the ethylene raw material gas E in the most downstream part is set for this pumping.

The flow controller 50 starts and stops the supply of the cleaning liquid W to the compression flow path R based on a pressure sensor (not shown) provided at the discharge port 3, and sets the detected value of the nozzle original pressure of each pressure sensor 52. Based on this, each motor-operated valve 51 is opened and closed to control the flow rate of the cleaning liquid W.

The flow controller 50 stores the ratio of the flow rate of the cleaning liquid W supplied to the first-stage radial spray body 21a, the second-stage return bend spray body 22a, and the third-stage return bend spray body 22a. is doing. This ratio decreases in the order of the first-stage radial spray body 21a, the second-stage return bend spray body 22a, and the third-stage return bend spray body 22a.
Further, the flow rate controller 50 is configured such that the total amount of the cleaning liquid W supplied to the compression flow path R per unit time is a predetermined ratio (3 by weight) with respect to the ethylene raw material gas E discharged from the discharge port 3. %), The total amount per unit time of the cleaning liquid W supplied to the compression flow path R is stored.

Then, the washing | cleaning method of the compression flow path R in the centrifugal compressor B is demonstrated.
First, when the ethylene raw material gas E continuously flows in the compression flow path R, the pressure of the ethylene raw material gas E discharged from the discharge port 3 decreases due to adhesion of the thermal decomposition product. Then, a detected value indicating this pressure is input to the flow rate controller 50 from a pressure sensor (not shown) provided at the discharge port 3.

The flow rate controller 50 opens and closes each motor-operated valve 51 so that the cleaning liquid W supplied to the stored compression flow path R is within the range of the total amount per unit time, so that the cleaning liquid W is supplied to the compression flow path R. Supply. At this time, the flow rate of the cleaning liquid W is controlled based on the detected value of the nozzle original pressure of each pressure sensor 52, the first-stage radial spray body 21 a, the second-stage return bend spray body 22 a, Control is performed so that the cleaning liquid W supplied to the third-stage return bend spray body 22a has a predetermined ratio. Specifically, the cleaning liquid W is controlled to increase in the order of the first-stage radial spray body 21a, the second-stage return bend spray body 22a, and the third-stage return bend spray body 22a.

That is, as described above, the adhesion amount of the polymer generated by the temperature rise of the ethylene source gas E is the largest in the first stage and decreases in the order of the second stage and the third stage. That is, a large amount of the cleaning liquid W is supplied to the first stage where the adhesion amount of the polymer is the largest, and a small amount is supplied in the order of the second stage and the third stage.
In this series of operations, the cleaning liquid W with respect to the ethylene source gas E per unit time discharged from the discharge port 3 is within a predetermined ratio (3% by weight) or less.

When the polymer is dissolved and flows downstream, the pressure of the ethylene raw material gas E discharged from the discharge port 3 is recovered. Then, the flow rate controller 50 closes the motor-operated valve 52 based on the detection value of a pressure sensor (not shown) provided at the discharge port 3 and stops the supply of the cleaning liquid W to the compression flow path R.
Thereafter, the centrifugal compressor B continues to operate stably.

As described above, according to the centrifugal compressor B, the flow rate controller 50 includes the first-stage radial spray body 21a, the second-stage return bend spray body 22a, and the third-stage return bend spray body. Since the spray amount of the cleaning liquid W is gradually reduced in the order of 22a, a large amount of the cleaning liquid W is sprayed on the upstream side where the temperature increase range of the ethylene raw material gas E is large and the thermal reaction product is large, and the downstream side where the temperature increase range is small A small amount of cleaning liquid W is sprayed on Accordingly, since the cleaning liquid W is sprayed according to the required amount of the cleaning liquid W in each part of the flow path of the ethylene raw material gas E, the mixing ratio of the cleaning liquid W to the ethylene raw material gas E without using the cleaning liquid W unnecessarily. Can be reduced.
In addition, since the flow controller 50 limits the total amount of the cleaning liquid W to a predetermined ratio with respect to the amount of the ethylene raw material gas E, the mixing ratio of the cleaning liquid W to the ethylene raw material gas E is limited to a predetermined range to achieve a desired quality. Ethylene raw material gas E can be obtained.

Instead of the above-described configuration, the pressure of each compression stage may be detected, and the cleaning liquid W may be supplied only to the stage where the pressure has decreased.
Further, in place of the above-described configuration, the pressure sensor is provided at the discharge port 3, but the cleaning liquid W may be supplied to the compression flow path R at regular intervals without providing the pressure sensor.

Note that the operation procedure shown in the above-described embodiment, various shapes and combinations of the constituent members, and the like are examples, and various modifications can be made based on design requirements and the like without departing from the gist of the present invention.
For example, in the above-described embodiment, the solvent is used for the cleaning liquid W, but water may be used instead. By doing in this way, a cooling effect can be increased.
In the above-described embodiment, the present invention is applied to the centrifugal compressors arranged in the back side. However, the present invention can also be applied to a type in which the directions of the impellers are unified in the axial direction.
In the above-described embodiment, the cleaning liquid W is sprayed from four locations in the circumferential direction. However, if there are two or more, the effect of the present invention can be sufficiently achieved.

DESCRIPTION OF SYMBOLS 1 ... Casing 1d ... Small diameter part 5 ... Rotating shaft 6 ... Impeller 14 ... Return bend channel | path (return bend part)
20 ... Cleaning fluid spraying device (cleaning fluid spraying device)
21 ... 1st spraying part (1st injection part)
21a: Radial spray body (radial spray body)
21b ... Axial spray body (axial spray body)
22 ... 2nd spraying part (2nd injection part)
22a ... return bend spray body (return bend spray body)
22b ... Oblique spray body (oblique spray body)
50 ... Flow controller (control unit)
A, B ... Centrifugal compressor E ... Ethylene feed gas (fluid)
P ... Axis R ... Compression flow path (flow path)
W ... Cleaning fluid

Claims

A casing, a rotating shaft supported in the casing, an impeller provided on the rotating shaft for compressing fluid, and a cleaning liquid ejecting apparatus for injecting a cleaning liquid into a flow path formed by the impeller and the casing. A centrifugal compressor,
The liquid ejection device includes a first ejection unit that ejects the cleaning liquid from a plurality of locations in a circumferential direction toward a gap between the small diameter portion of the casing and the impeller.
A centrifugal compressor comprising: a second injection unit that injects the cleaning liquid from a plurality of locations in the circumferential direction from the upstream side to the downstream side of the fluid compressed by the impeller.
The centrifugal compressor according to claim 1, wherein the first injection unit includes a radial injection body that injects the cleaning liquid in a radial direction toward the gap.
The tip position of the first injection unit is radially arranged in the outer peripheral side of the impeller, and the first injection unit is an axial injection unit that injects the cleaning liquid in the axial direction toward the gap. The centrifugal compressor according to claim 1 or 2 provided.
2. The centrifugal compression according to claim 1, wherein the second injection unit includes an oblique injection body that injects the cleaning liquid in a direction obliquely intersecting with the fluid that flows radially outward from the outermost peripheral portion of the impeller. Machine.
A plurality of the impellers are provided in the axial direction;
The casing is formed with a return bend portion for directing the fluid flowing radially outward from the upstream impeller to the downstream impeller adjacent to the upstream impeller, and the fluid is compressed in multiple stages. And
2. The centrifugal compressor according to claim 1, wherein the second injection unit includes a return bend injection body that is provided on a downstream side of the return bend unit and injects the cleaning liquid inward in a radial direction.
The centrifugal compressor according to claim 1, wherein at least one of the first injection unit and the second injection unit sprays the cleaning liquid.
Each of the plurality of impellers in a casing, a rotating shaft supported in the casing, a plurality of impellers provided on the rotating shaft to compress fluid, and a flow path formed by the plurality of impellers and the casing A centrifugal compressor provided with a plurality of injectors provided on the upstream side for injecting a cleaning liquid, and a control unit for adjusting each injection amount of these injectors,
The said control part is a centrifugal compressor which reduces each said injection quantity gradually toward the said injection body located downstream from the said injection body located in an upstream.
The centrifugal compressor according to claim 7, wherein the control unit limits a total amount of the cleaning liquid ejected from each of the ejectors to a predetermined ratio with respect to the amount of the fluid.